JP7553265B2 - Porous ceramic laminate and manufacturing method thereof - Google Patents
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Description
本発明は多孔質セラミックス積層体及びその製造方法に関する。 The present invention relates to a porous ceramic laminate and a method for manufacturing the same.
多孔質セラミックスは、精密濾過膜、限外濾過膜、ナノ濾過膜、逆浸透膜、イオン交換膜、ガス分離膜等、気体、液体等の流体の分離、濃縮、濾過等の機能を有する膜として、様々な分野で利用されている。 Porous ceramics are used in a variety of fields as membranes with functions such as separating, concentrating, and filtering gases, liquids, and other fluids, including microfiltration membranes, ultrafiltration membranes, nanofiltration membranes, reverse osmosis membranes, ion exchange membranes, and gas separation membranes.
例えば、特許文献1には、無機質支持体と、前記支持体を被覆する1層以上の無機質被覆層から成るセラミック多孔質非対称膜であって、前記支持体を被覆する1層以上の無機質被覆層のうちの少なくとも1層として、薄層状の無機多孔質体を含むセラミック多孔体が開示されている。特許文献1では、平均細孔径が11.0又は14.2μmの多孔質支持体に、平均粒子径が3又は5μmのアルミナを含むスラリー膜を製膜し、焼成して、前記多孔質支持体上に多孔質層を形成している。また、特許文献2には、支持層と、その支持層の内面或いは外面に形成される多孔質層からなる非対称膜が開示されている。特許文献2では、平均粒子径5μmのアルミナ粒子やその他の無機物質の粒子を用いて連通気孔径1~2μmの支持層を作成し、平均粒径0.5μmのアルミナ微粉末が分散した液を用いて前記支持層の表面に多孔質層を形成している。 For example, Patent Document 1 discloses a ceramic porous asymmetric membrane consisting of an inorganic support and one or more inorganic coating layers covering the support, in which at least one of the one or more inorganic coating layers covering the support contains a thin-layered inorganic porous body. In Patent Document 1, a slurry membrane containing alumina with an average particle size of 3 or 5 μm is formed on a porous support having an average pore size of 11.0 or 14.2 μm, and the porous layer is formed on the porous support by firing. Patent Document 2 discloses an asymmetric membrane consisting of a support layer and a porous layer formed on the inner or outer surface of the support layer. In Patent Document 2, a support layer with a pore size of 1 to 2 μm is created using alumina particles with an average particle size of 5 μm or particles of other inorganic substances, and a porous layer is formed on the surface of the support layer using a liquid in which alumina fine powder with an average particle size of 0.5 μm is dispersed.
多孔質セラミックスを用いて、流体の分離等を行う場合、分離等の機能を十分に発揮しつつ、前記セラミックス多孔体中に流体が流れやすいこと、すなわち流体の圧力損失が小さいことが重要であるが、前記特許文献1及び2では、流体の圧力損失を低減することが難しいと考えられる。 When using porous ceramics to separate fluids, it is important that the fluid flows easily through the porous ceramics while still fully performing the function of separation, i.e., that the pressure loss of the fluid is small. However, it is considered difficult to reduce the pressure loss of the fluid in Patent Documents 1 and 2.
そこで、本発明は、流体の圧力損失を低減できる多孔質セラミックス積層体を提供することを目的とする。 Therefore, the present invention aims to provide a porous ceramic laminate that can reduce fluid pressure loss.
上記課題を達成した本発明は以下の通りである。
[1]第1多孔質層と、前記第1多孔質層の上に積層された第2多孔質層とを有する多孔質セラミックス積層体であって、
前記第2多孔質層は、前記第1多孔質層の上に接して積層されている部分と、前記第1多孔質層の上に空気を介して積層されている部分を有し、
前記第2多孔質層の膜厚の変動係数CV(tb)が0.35以下であることを特徴とする多孔質セラミックス積層体。
[2]前記第1多孔質層の平均細孔径Daが0.1μm以上、600μm以下である[1]に記載の多孔質セラミックス積層体。
[3]前記第2多孔質層の膜厚の標準偏差σ(tb)を、前記第1多孔質層の平均細孔径Daで除した値(σ(tb)/Da)が0.8以下である[1]または[2]に記載の多孔質セラミックス積層体。
[4]前記第2多孔質層の膜厚の平均値AVE(tb)を、前記第1多孔質層の平均細孔径Daで除した値(AVE(tb)/Da)が5以下である[1]~[3]のいずれかに記載の多孔質セラミックス積層体。
[5]前記第1多孔質層と前記第2多孔質層の界面における空隙率が29.0%以上である[1]~[4]のいずれかに記載の多孔質セラミックス積層体。
[6]前記第2多孔質層の平均細孔径Dbに対する前記第1多孔質層の平均細孔径Daの比(Da/Db)が10以上である[1]~[5]のいずれかに記載の多孔質セラミックス積層体。
[7][1]~[6]のいずれかに記載の多孔質セラミックス積層体の製造方法であって、
前記第1多孔質層の少なくとも一方の表面に、撥水剤及び/又は撥油剤を塗布する工程を含み、
前記撥水剤及び/又は撥油剤は、下記の条件(1)及び(2)が満たされるように塗布される多孔質セラミックス積層体の製造方法。
(1)撥水剤及び/又は撥油剤を前記第1多孔質層の少なくとも一方の表面に塗布し、乾燥後、前記第1多孔質層の撥水剤及び/又は撥油剤塗布面(両面に塗布される場合にはいずれか一方の塗布面)から空気を1.0m3/hの流量で流した際、空気を流した面と反対側の面から少なくとも0.8m3/h以上の流量の空気が流れる。
(2)撥水剤及び/又は撥油剤を前記第1多孔質層の少なくとも一方の表面に塗布し、乾燥後、前記第1多孔質層の撥水剤及び/又は撥油剤塗布面(両面に塗布される場合にはいずれか一方の塗布面)から空気を1.0m3/hの流量で流した際、空気を流す試験前後の重量減少率が0.1%以内である。
The present invention which achieves the above object is as follows.
[1] A porous ceramic laminate having a first porous layer and a second porous layer laminated on the first porous layer,
the second porous layer has a portion laminated on and in contact with the first porous layer and a portion laminated on the first porous layer with air interposed therebetween;
A porous ceramic laminate, wherein the coefficient of variation CV(t b ) of the thickness of the second porous layer is 0.35 or less.
[2] The porous ceramic laminate according to [1], wherein the average pore diameter D a of the first porous layer is 0.1 μm or more and 600 μm or less.
[3] A porous ceramic laminate according to [1] or [2], wherein the value (σ(t b )/D a ) obtained by dividing the standard deviation σ(t b ) of the thickness of the second porous layer by the average pore diameter D a of the first porous layer is 0.8 or less.
[4] A porous ceramic laminate according to any one of [1] to [3], wherein the value (AVE(t b )/D a ) obtained by dividing the average thickness AVE(t b ) of the second porous layer by the average pore diameter D a of the first porous layer is 5 or less.
[5] The porous ceramic laminate according to any one of [1] to [4], wherein the porosity at the interface between the first porous layer and the second porous layer is 29.0% or more.
[6] The porous ceramic laminate according to any one of [1] to [5], wherein the ratio (D a /D b ) of the average pore diameter D a of the first porous layer to the average pore diameter D b of the second porous layer is 10 or more.
[7] A method for producing a porous ceramic laminate according to any one of [1] to [6],
A step of applying a water repellent and/or an oil repellent to at least one surface of the first porous layer,
The method for producing a porous ceramic laminate, wherein the water repellent and/or oil repellent is applied so as to satisfy the following conditions (1) and (2):
(1) A water-repellent and/or oil-repellent is applied to at least one surface of the first porous layer, and after drying, when air is caused to flow at a flow rate of 1.0 m3 /h from the water-repellent and/or oil-repellent coated surface of the first porous layer (or from either one of the coated surfaces if coated on both surfaces), air flows at a flow rate of at least 0.8 m3 /h from the surface opposite to the surface through which the air is flowing.
(2) When a water-repellent and/or oil-repellent is applied to at least one surface of the first porous layer and dried, and then air is caused to flow at a flow rate of 1.0 m3 /h from the water-repellent and/or oil-repellent coated surface of the first porous layer (or from either one of the coated surfaces if coated on both surfaces), the weight loss rate before and after the air flow test is within 0.1%.
本発明の多孔質セラミックス積層体は、気体、液体等の流体の圧力損失を低減できる。 The porous ceramic laminate of the present invention can reduce pressure loss of fluids such as gases and liquids.
本発明の多孔質セラミックス積層体は、第1多孔質層と、前記第1多孔質層の上に積層された第2多孔質層とを有する多孔質セラミックス積層体であって、前記第2多孔質層は、前記第1多孔質層の上に接して積層されている部分と、前記第1多孔質層の上に空気を介して積層されている部分を有し、前記第2多孔質層の膜厚の変動係数CV(tb)が0.35以下であることを特徴とする。 The porous ceramic laminate of the present invention is a porous ceramic laminate having a first porous layer and a second porous layer laminated on the first porous layer, wherein the second porous layer has a portion laminated in contact with the first porous layer and a portion laminated on the first porous layer with air between them, and is characterized in that the coefficient of variation CV(t b ) of the film thickness of the second porous layer is 0.35 or less.
前記第2多孔質層の一部は、前記第1多孔質層の上に接して積層されており、前記第2多孔質層のその他の部分は、空気を介して前記第1多孔質層の上に積層されており、前記第2多孔質層が、空気を介して前記第1多孔質層の上に積層されている箇所を有することは、流体の圧力損失を低減する上で重要な要件である。 A part of the second porous layer is laminated on top of the first porous layer in contact with it, and the other part of the second porous layer is laminated on the first porous layer via air. The fact that the second porous layer has a portion laminated on the first porous layer via air is an important requirement for reducing pressure loss of the fluid.
更に、前記多孔質セラミックス積層体において、第2多孔質層の膜厚の変動係数CV(tb)が0.35以下となるように均一に形成されることで、多孔質セラミックス積層体中に流れる流体の圧力損失を低減できる。前記第2多孔質層の膜厚tbの変動係数CV(tb)は、0.32以下が好ましく、0.25以下がより好ましく、0.20以下が更に好ましい。前記変動係数の下限は特に限定されないが、例えば0.05であり、0.10であってもよい。なお、前記膜厚tbは以下の要領で測定することができ、また前記膜厚の変動係数CV(tb)は、膜厚の標準偏差σ(tb)を膜厚の平均値AVE(tb)で除すことにより求めることができる。まず、前記第1多孔質層と第2多孔質層の積層方向に平行な断面の画像を取得する。前記画像において、前記第2多孔質層の、第1多孔質層側表面の合計長さが、前記第1多孔質層の平均細孔径の100倍以上となるように画像を取得して、画像解析により第2多孔質層のみを抽出する。そして、得られた画像を一定間隔で区切って190か所以上の領域とし、各領域の面積を求めて、区切った間隔の長さで除した値を各領域における第2多孔質層の膜厚とし、測定した全領域についての膜厚の平均値、標準偏差、変動係数を求める。ただし、区切った間隔の長さは第1多孔質層の平均細孔径の1.8倍以下の長さとする。 Furthermore, in the porous ceramic laminate, the coefficient of variation CV(t b ) of the thickness of the second porous layer is uniformly formed to be 0.35 or less, thereby reducing the pressure loss of the fluid flowing through the porous ceramic laminate. The coefficient of variation CV(t b ) of the thickness t b of the second porous layer is preferably 0.32 or less, more preferably 0.25 or less, and even more preferably 0.20 or less. The lower limit of the coefficient of variation is not particularly limited, but may be, for example, 0.05 or 0.10. The thickness t b can be measured as follows, and the coefficient of variation CV(t b ) of the thickness can be obtained by dividing the standard deviation σ(t b ) of the thickness by the average thickness AVE(t b ). First, an image of a cross section parallel to the lamination direction of the first porous layer and the second porous layer is obtained. In the image, the total length of the surface of the second porous layer on the side of the first porous layer is 100 times or more the average pore diameter of the first porous layer, and only the second porous layer is extracted by image analysis. The obtained image is divided at regular intervals into 190 or more regions, the area of each region is calculated, and the value divided by the length of the divided interval is regarded as the film thickness of the second porous layer in each region, and the average value, standard deviation, and coefficient of variation of the film thickness for all the measured regions are calculated. However, the length of the divided interval is 1.8 times or less the average pore diameter of the first porous layer.
前記膜厚の変動係数CV(tb)が0.35以下である限り、前記第2多孔質層の膜厚の平均値AVE(tb)は限定されないが、平均値AVE(tb)は例えば0.3μm以上であり、より好ましくは1.0μm以上、更に好ましくは5.0μm以上、一層好ましくは10μm以上であり、また例えば3000μm以下であり、500μm以下がより好ましく、更に好ましくは100μm以下であり、一層好ましくは75μm以下であり、特に50μm以下が好ましい。また、平均値AVE(tb)は、15μm以上、25μm以下の範囲であってもよい。 As long as the coefficient of variation CV(t b ) of the thickness is 0.35 or less, the average value AVE(t b ) of the thickness of the second porous layer is not limited, but the average value AVE(t b ) is, for example, 0.3 μm or more, more preferably 1.0 μm or more, even more preferably 5.0 μm or more, even more preferably 10 μm or more, and for example, 3000 μm or less, more preferably 500 μm or less, even more preferably 100 μm or less, even more preferably 75 μm or less, and particularly preferably 50 μm or less. The average value AVE(t b ) may be in the range of 15 μm or more and 25 μm or less.
また、前記第2多孔質層の膜厚の標準偏差σ(tb)を前記第1多孔質層の平均細孔径Daで除した値(σ(tb)/Da)を調整することも好ましい。σ(tb)/Daは0.8以下であることが好ましく、0.6以下がより好ましく、0.5以下が更に好ましく、0.4以下が一層好ましい。σ(tb)/Daの下限は特に限定されないが、0.2程度であってもよい。σ(tb)/Daは、第一多孔質層の平均細孔径に対する第2多孔質層膜厚標準偏差を表し、当該値は小さいほど、第2多孔質層が均一に塗工できている事を表しており、圧力損失を低減する観点から、σ(tb)/Daは小さい方が好ましい。 It is also preferable to adjust the value (σ(t b )/D a ) obtained by dividing the standard deviation σ(t b ) of the thickness of the second porous layer by the average pore diameter D a of the first porous layer. σ(t b )/D a is preferably 0.8 or less, more preferably 0.6 or less, even more preferably 0.5 or less, and even more preferably 0.4 or less. The lower limit of σ(t b )/D a is not particularly limited, but may be about 0.2. σ(t b )/D a represents the standard deviation of the thickness of the second porous layer relative to the average pore diameter of the first porous layer, and the smaller this value is, the more uniformly the second porous layer can be coated. From the viewpoint of reducing pressure loss, it is preferable that σ(t b )/D a is smaller.
更に、前記第2多孔質層の膜厚の平均値AVE(tb)を、前記第1多孔質層の平均細孔径Daで除した値(AVE(tb)/Da)が5以下であることも好ましく、好ましくは4以下であり、更に好ましくは3以下であり、下限は特に限定されないが例えば0.5程度であってもよい。 Furthermore, it is also preferable that the value (AVE(t b )/D a ) obtained by dividing the average thickness AVE(t b ) of the second porous layer by the average pore diameter Da of the first porous layer is 5 or less, preferably 4 or less, and more preferably 3 or less. The lower limit is not particularly limited, but may be, for example, about 0.5.
流体の圧力損失を低減する観点から、前記第1多孔質層と前記第2多孔質層の界面における空隙率を所定以上にすることも好ましい。前記空隙率は、以下の要領で求めることができる。まず、前記第1多孔質層と第2多孔質層の積層方向に平行な断面の画像を取得する。前記画像において、前記第2多孔質層の、第1多孔質層側表面の合計長さが、前記第1多孔質層の平均細孔径の250倍以上となるように画像を取得して、画像解析により第2多孔質層のみを抽出する。抽出した第2多孔質層の下側(第2多孔質層の、第1多孔質層側表面から第1多孔質層側)の領域について、前記第2多孔質層の前記第1多孔質層側の境界から、第2多孔質層に沿って、第1多孔質層の細孔径の2倍の領域を画像解析により設定し、解析領域とする。この解析領域内の空隙部分を画像解析で抽出し、空隙部分の面積を解析領域の面積で除算して100倍することで空隙率を得ることができる。 From the viewpoint of reducing the pressure loss of the fluid, it is also preferable to set the porosity at the interface between the first porous layer and the second porous layer to a predetermined value or more. The porosity can be obtained as follows. First, an image of a cross section parallel to the lamination direction of the first porous layer and the second porous layer is obtained. In the image, an image is obtained so that the total length of the first porous layer side surface of the second porous layer is 250 times or more the average pore diameter of the first porous layer, and only the second porous layer is extracted by image analysis. For the region below the extracted second porous layer (from the first porous layer side surface of the second porous layer to the first porous layer side), a region twice the pore diameter of the first porous layer is set by image analysis along the second porous layer from the boundary of the second porous layer on the first porous layer side, and set as the analysis region. The void portion in this analysis region is extracted by image analysis, and the area of the void portion is divided by the area of the analysis region and multiplied by 100 to obtain the porosity.
前記空隙率は29.0%以上であることが好ましく、より好ましくは30%以上であり、更に好ましくは33%以上である。前記空隙率の上限は、前記第1多孔質層の空隙率にもよるが、例えば55%である。 The porosity is preferably 29.0% or more, more preferably 30% or more, and even more preferably 33% or more. The upper limit of the porosity depends on the porosity of the first porous layer, but is, for example, 55%.
また、前記第2多孔質層の平均細孔径Dbに対する前記第1多孔質層の平均細孔径Daの比(Da/Db)が10以上であることが好ましい。このように、DaとDbの差を大きくすることで、前記多孔質セラミックス積層体を透過する流体の圧力損失をより低減することができるため好ましい。Da/Dbは、好ましくは10以上、200以下であり、より好ましくは10以上、150以下であり、更に好ましくは15以上、100以下であり、一層好ましくは20以上(特に50以上)、65以下である。なお、前記特許文献1では、平均粒子径が3又は5μmのアルミナを含むスラリーを用いて、前記多孔質支持体上に前記多孔質層を形成しており、前記アルミナの粒子径から考えて、前記多孔質層の平均細孔径は1μm程度と考えられ、前述した通り、前記多孔質支持体の平均細孔径は11.0又は14.2μmである。従って、前記特許文献1における前記多孔質層の平均細孔径に対する前記支持体の平均細孔径の比は、最大でも14程度であると考えられる。また、特許文献2では、前記支持層の連通気孔径が1~2μmであり、前記多孔質層の気孔径が0.2μmであるため、前記多孔質層の気孔径に対する前記支持層の連通気孔径の比は最大でも10である。 In addition, the ratio (D a /D b ) of the average pore diameter D a of the first porous layer to the average pore diameter D b of the second porous layer is preferably 10 or more. In this way, by increasing the difference between Da and Db, the pressure loss of the fluid passing through the porous ceramic laminate can be further reduced, which is preferable. D a /D b is preferably 10 or more and 200 or less, more preferably 10 or more and 150 or less, even more preferably 15 or more and 100 or less, and even more preferably 20 or more (particularly 50 or more) and 65 or less. In addition, in the above-mentioned Patent Document 1, the porous layer is formed on the porous support using a slurry containing alumina having an average particle diameter of 3 or 5 μm, and considering the particle diameter of the alumina, the average pore diameter of the porous layer is considered to be about 1 μm, and as described above, the average pore diameter of the porous support is 11.0 or 14.2 μm. Therefore, the ratio of the average pore diameter of the support to the average pore diameter of the porous layer in the above-mentioned Patent Document 1 is considered to be about 14 at most. In addition, in Patent Document 2, the support layer has an interconnected pore size of 1 to 2 μm, and the porous layer has a pore size of 0.2 μm, so the ratio of the interconnected pore size of the support layer to the pore size of the porous layer is 10 at most.
前記第1多孔質層の平均細孔径Daは、例えば0.1μm以上であり、好ましくは1.0μm以上、より好ましくは1.5μm以上、更に好ましくは5μm以上、一層好ましくは9μm以上であり、また600μm以下であってもよく、好ましくは300μm以下であり、より好ましくは60μm以下である。Daは12μm以上、18μmの範囲であってもよい。また、前記第2多孔質層の平均細孔径Dbは例えば0.01μm以上、10μm以下であり、好ましくは0.05μm以上、5μm以下であり、より好ましくは0.15μm以上、1μm以下であり、更に好ましくは0.20μm以上、1μm以下である。 The average pore diameter D a of the first porous layer is, for example, 0.1 μm or more, preferably 1.0 μm or more, more preferably 1.5 μm or more, even more preferably 5 μm or more, even more preferably 9 μm or more, and may be 600 μm or less, preferably 300 μm or less, and more preferably 60 μm or less. D a may be in the range of 12 μm or more and 18 μm. The average pore diameter D b of the second porous layer is, for example, 0.01 μm or more and 10 μm or less, preferably 0.05 μm or more and 5 μm or less, more preferably 0.15 μm or more and 1 μm or less, and even more preferably 0.20 μm or more and 1 μm or less.
前記第1多孔質層の平均厚みは、例えば500μm以上、5000μm以下であり、好ましくは1000μm以上、2800μm以下、さらに好ましくは1400μm以上、1900μm以下である。 The average thickness of the first porous layer is, for example, 500 μm or more and 5000 μm or less, preferably 1000 μm or more and 2800 μm or less, and more preferably 1400 μm or more and 1900 μm or less.
前記第2多孔質層は、前記第1多孔質層の少なくとも片面に積層されていればよく、前記第1多孔質層の片面のみに積層されていることが好ましい。本発明の多孔質セラミックス積層体の形状は特に限定されず、平面状、円筒状、又はハニカム状であってもよく、円筒状であることが好ましい。本発明の多孔質セラミックス積層体が円筒状である場合、前記第2多孔質層は、前記第1多孔質層の外周面又は内周面のいずれに積層されていてもよく、前記第1多孔質層の外周面のみ又は内周面のみに積層されていることが好ましく、前記第1多孔質層の外周面のみに前記第2多孔質層が積層されていることがより好ましい。 The second porous layer may be laminated on at least one side of the first porous layer, and is preferably laminated on only one side of the first porous layer. The shape of the porous ceramic laminate of the present invention is not particularly limited, and may be planar, cylindrical, or honeycomb, and is preferably cylindrical. When the porous ceramic laminate of the present invention is cylindrical, the second porous layer may be laminated on either the outer peripheral surface or the inner peripheral surface of the first porous layer, and is preferably laminated only on the outer peripheral surface or the inner peripheral surface of the first porous layer, and it is more preferable that the second porous layer is laminated only on the outer peripheral surface of the first porous layer.
前記第1多孔質層及び第2多孔質層の素材は特に限定されないが、いずれも金属酸化物を含むことが好ましい。なお、本発明において、金属とは、Si、Ge等の半金属を含む意味で用いる。前記第1多孔質層は、前記金属酸化物として、金属酸化物A及び前記金属酸化物Aの融点よりも高い融点を有する金属酸化物Bを含むことが好ましく、前記第2多孔質層は、前記金属酸化物として、前記金属酸化物Aの融点よりも高い融点を有する金属酸化物Cを含むことが好ましい。前記金属酸化物B及び前記金属酸化物Cは同一であってもよく異なっていてもよい。 The materials of the first and second porous layers are not particularly limited, but it is preferable that both contain a metal oxide. In the present invention, the term "metal" is used to mean a metalloid such as Si or Ge. The first porous layer preferably contains, as the metal oxide, a metal oxide A and a metal oxide B having a melting point higher than that of the metal oxide A, and the second porous layer preferably contains, as the metal oxide, a metal oxide C having a melting point higher than that of the metal oxide A. The metal oxide B and the metal oxide C may be the same or different.
前記金属酸化物Aは融点が95℃以上、1600℃以下であることが好ましい。前記金属酸化物Aとしては、具体的には、B2O3、SiO2、GeO2、Al2O3、V2O5、As2O5、Sb2O5、ZrO2、TiO2、ZnO、PbO、ThO2、BeO、CdO、Ta2O5、Nb2O5、WO3、ScO2、La2O3、Y2O3、SnO2、Ga2O3、In2O3、PbO2、MgO、Li2O、BaO、CaO、SrO、Na2O、K2O、Rb2O、HgO、Cs2O、Ag2O、TeO2、Tl2O等が挙げられ、好ましくはSiO2が挙げられる。つまり、前記金属酸化物Aは、前記した酸化物の少なくとも1種を構成成分とするものが挙げられ、特に前記した酸化物の少なくとも1つを構成成分とするガラスであることが好ましく、特に石英ガラス、ホウケイ酸ガラス、アルミナケイ酸塩ガラス等のケイ素の酸化物(特にSiO2)を含むガラスであることが好ましい。前記金属酸化物B及び前記金属酸化物Cは、同一であっても異なっていてもよく、いずれも融点が2000℃以上、2800℃以下であることが好ましい。前記金属酸化物B及び前記金属酸化物Cとしては、具体的には、Al2O3、ZrO2、MgO、Cr2O3、Y2O3等が挙げられ、好ましくはAl2O3が挙げられる。 The metal oxide A preferably has a melting point of 95° C. or higher and 1600° C. or lower. Specific examples of the metal oxide A include B2O3 , SiO2 , GeO2 , Al2O3 , V2O5 , As2O5 , Sb2O5 , ZrO2 , TiO2 , ZnO , PbO, ThO2 , BeO , CdO, Ta2O5 , Nb2O5 , WO3 , ScO2 , La2O3 , Y2O3 , SnO2 , Ga2O3 , In2O3 , PbO2 , MgO , Li2O , BaO, CaO , SrO , Na2O , K2O , Rb2O, HgO, Cs2O , and Ag . 2O , TeO2 , Tl2O , etc., preferably SiO2 . That is, the metal oxide A may be one having at least one of the above oxides as a constituent, and is preferably a glass having at least one of the above oxides as a constituent, and is preferably a glass containing an oxide of silicon (particularly SiO2 ), such as quartz glass, borosilicate glass, or alumina silicate glass. The metal oxide B and the metal oxide C may be the same or different, and each preferably has a melting point of 2000°C or more and 2800°C or less. Specific examples of the metal oxide B and the metal oxide C include Al2O3 , ZrO2 , MgO , Cr2O3 , Y2O3 , etc. , and is preferably Al2O3 .
前記多孔質セラミックス積層体は、前記第1及び第2多孔質層に加えて、更に第2多孔質層の上に、1層以上の他の多孔質層が更に積層されていてもよい。前記他の多孔質層は前記第2多孔質層よりも平均細孔径が小さいことが好ましく、他の多孔質層が2層以上ある場合には、前記第2多孔質層に最も近い他の多孔質層の平均細孔径が最も大きく、積層されるに従って平均細孔径が小さくなる構成とすることが好ましい。 In addition to the first and second porous layers, the porous ceramic laminate may further include one or more other porous layers laminated on the second porous layer. The other porous layers preferably have a smaller average pore diameter than the second porous layer, and when there are two or more other porous layers, it is preferable that the average pore diameter of the other porous layer closest to the second porous layer is the largest, and the average pore diameter decreases as the layers are laminated.
本発明の多孔質セラミックス積層体は、流体の圧力損失を低減することができる。前記多孔質セラミックス積層体は、後記する実施例で評価されるパーミアンスを5.0×10-5mol/(m2・sec・Pa)以上にすることができ、好ましくは1.0×10-4mol/(m2・sec・Pa)以上とすることができ、より好ましくは1.5×10-4mol/(m2・sec・Pa)以上とすることができる。前記パーミアンスの上限は特に限定されないが、例えば1.5×10-3mol/(m2・sec・Pa)であり、5.0×10-4mol/(m2・sec・Pa)であってもよい。 The porous ceramic laminate of the present invention can reduce the pressure loss of a fluid. The porous ceramic laminate can have a permeance evaluated in the examples described below of 5.0×10 −5 mol/(m 2 ·sec·Pa) or more, preferably 1.0×10 −4 mol/(m 2 ·sec·Pa) or more, and more preferably 1.5×10 −4 mol/(m 2 ·sec·Pa) or more. The upper limit of the permeance is not particularly limited, but may be, for example, 1.5×10 −3 mol/(m 2 ·sec·Pa) or 5.0×10 −4 mol/(m 2 ·sec·Pa).
次に、前記多孔質セラミックス積層体の製造方法について説明する。通常、多孔質層の上に他の層を積層させようとすると、基材となる多孔質層(第1多孔質層)の細孔内に、上の層(第2多孔質層)の構成成分が取り込まれるため、第2多孔質層を層状に形成することが難しい上に、更に膜厚の均一性の高い第2多孔質層を形成することは難しい。 Next, a method for manufacturing the porous ceramic laminate will be described. Normally, when attempting to laminate another layer on a porous layer, the components of the upper layer (second porous layer) are incorporated into the pores of the porous layer (first porous layer) that serves as the base material, making it difficult to form the second porous layer in a layered form, and furthermore, it is difficult to form a second porous layer with a highly uniform film thickness.
前記多孔質セラミックス積層体の製造方法は、前記第1多孔質層の少なくとも一方の表面に、撥水剤及び/又は撥油剤を塗布する工程を含む。前記撥水剤及び/又は撥油剤を塗布することで、その後に塗布される第2多孔質層の構成成分が、第多孔質層の細孔内に取り込まれることがないため、第1多孔質層の上に、層状でかつ膜厚の均一性の高い第2多孔質層を形成することができる。上記した「表面」とは、多孔質体の表面に存在する孔も含める意味であり、撥水剤及び/又は撥油剤はこの孔も含めて多孔質体の少なくとも一方の表面に塗布される。ここで、撥水剤又は撥油剤は、以下の条件(1)及び(2)が満たされるように塗布される。 The method for manufacturing the porous ceramic laminate includes a step of applying a water repellent and/or oil repellent to at least one surface of the first porous layer. By applying the water repellent and/or oil repellent, the components of the second porous layer to be applied thereafter are not taken into the pores of the first porous layer, so that a second porous layer having a laminar shape and a highly uniform thickness can be formed on the first porous layer. The above-mentioned "surface" includes the pores present on the surface of the porous body, and the water repellent and/or oil repellent is applied to at least one surface of the porous body including the pores. Here, the water repellent or oil repellent is applied so that the following conditions (1) and (2) are satisfied.
(1)撥水剤及び/又は撥油剤を前記第1多孔質層の少なくとも一方の表面に塗布し、乾燥後、前記第1多孔質層の撥水剤及び/又は撥油剤塗布面(両面に塗布される場合にはいずれか一方の塗布面)から空気を1.0m3/hの流量で流した際、空気を流した面と反対側の面から少なくとも0.8m3/h以上の流量の空気が流れる。
(2)撥水剤及び/又は撥油剤を前記第1多孔質層体の少なくとも一方の表面に塗布し、乾燥後、前記第1多孔質層の撥水剤及び/又は撥油剤塗布面(両面に塗布される場合にはいずれか一方の塗布面)から空気を1.0m3/hの流量で流した際、空気を流す試験前後の重量減少率が0.1%以内である。
(1) A water-repellent and/or oil-repellent is applied to at least one surface of the first porous layer, and after drying, when air is caused to flow at a flow rate of 1.0 m3 /h from the water-repellent and/or oil-repellent coated surface of the first porous layer (or from either one of the coated surfaces if coated on both surfaces), air flows at a flow rate of at least 0.8 m3 /h from the surface opposite to the surface through which the air is flowing.
(2) When a water-repellent and/or oil-repellent is applied to at least one surface of the first porous layer body and dried, and then air is passed through the water-repellent and/or oil-repellent-coated surface of the first porous layer (or through either one of the coated surfaces if coated on both surfaces) at a flow rate of 1.0 m3 /h, the weight loss rate before and after the air passage test is within 0.1%.
つまり、撥水剤及び/又は撥油剤塗布後の第1多孔質層に所定流量の空気を流したときに、通気が確保され、かつ撥水剤及び/又は撥油剤が第1多孔質層から離脱しないように、撥水剤及び/又は撥油剤が塗布されていることが重要である。 In other words, it is important that the water repellent and/or oil repellent is applied so that when a predetermined flow rate of air is passed through the first porous layer after the water repellent and/or oil repellent is applied, ventilation is ensured and the water repellent and/or oil repellent does not separate from the first porous layer.
上記条件(1)について、撥水剤及び/又は撥油剤が第1多孔質層の片面に塗布されている時には、撥水剤及び/又は撥油剤の塗布面から空気を流し、その反対側面での空気の流量を測定すればよく、両面に塗布されている場合には、いずれか一方の塗布面から空気を流して、その反対側面での空気の流量を測定すればよい。上記条件(1)の空気を流す時間は、3分であり、流す空気の温度は10~35℃である。 Regarding the above condition (1), when the water repellent and/or oil repellent is applied to one side of the first porous layer, air is allowed to flow from the side to which the water repellent and/or oil repellent is applied and the air flow rate on the opposite side is measured. When the water repellent and/or oil repellent are applied to both sides, air is allowed to flow from one of the applied sides and the air flow rate on the opposite side is measured. The time for which the air is allowed to flow under the above condition (1) is 3 minutes, and the temperature of the air being allowed to flow is 10 to 35°C.
また、上記条件(2)については、撥水剤及び/又は撥油剤が第1多孔質層の片面に塗布されている時には、撥水剤及び/又は撥油剤の塗布面から空気を流し、また両面に塗布されている場合には、いずれか一方の塗布面から空気を流して、重量減少率を測定すればよい。重量減少率は、撥水剤及び/又は撥油剤が塗布され空気を流す前の第1多孔質層重量から、空気を流した後の第1多孔質層重量を差し引き、これを、空気を流す前の第1多孔質層重量で除した割合(百分率)である。 Regarding the above condition (2), when the water repellent and/or oil repellent is applied to one side of the first porous layer, air is allowed to flow from the surface to which the water repellent and/or oil repellent is applied, and when the water repellent and/or oil repellent are applied to both sides, air is allowed to flow from either one of the surfaces to measure the weight reduction rate. The weight reduction rate is the ratio (percentage) obtained by subtracting the weight of the first porous layer after air has been allowed to flow from the weight of the first porous layer before air is allowed to flow, by the weight of the first porous layer before air is allowed to flow.
撥水剤及び/又は撥油剤の塗布方法としては、ディップコートが好ましく、撥水剤及び/又は撥油剤の塗布後は、通常乾燥を行う。乾燥は、20~50℃程度で1分~24時間程度行うことが好ましい。また、撥水剤及び/又は撥油剤の塗布及び乾燥後に、撥水剤及び/撥油剤が残存していることが好ましい。上記条件(1)及び(2)を満足できる限り、撥水剤及び撥油剤の組成は限定されないが、例えばフッ素系撥水撥油剤、ポリシロキサン系撥水撥油剤を用いることができる。フッ素系撥水撥油剤としては、パーフルオロアルキル基を有するもの、パーフルオロポリエーテル構造を有するものなどが挙げられる。 The preferred method for applying the water and/or oil repellent is dip coating, and after application of the water and/or oil repellent, drying is usually performed. Drying is preferably performed at about 20 to 50°C for about 1 minute to 24 hours. It is also preferred that the water and/or oil repellent remains after application and drying. As long as the above conditions (1) and (2) are satisfied, the composition of the water and oil repellent is not limited, but for example, fluorine-based water and oil repellents and polysiloxane-based water and oil repellents can be used. Examples of fluorine-based water and oil repellents include those having a perfluoroalkyl group and those having a perfluoropolyether structure.
前記製造方法において、更に、前記撥水剤又は前記撥油剤が塗布された前記第1多孔質層の表面に、前記第2多孔質層に含まれる前記金属酸化物と溶剤と増粘剤を含むスラリーを塗布する工程、及び前記スラリーが塗布された前記第1多孔質層を熱処理する工程を含むことが好ましい。 It is preferable that the manufacturing method further includes a step of applying a slurry containing the metal oxide contained in the second porous layer, a solvent, and a thickener to the surface of the first porous layer to which the water repellent or the oil repellent has been applied, and a step of heat treating the first porous layer to which the slurry has been applied.
前記溶剤としては、水、有機系溶剤等が挙げられる。好ましい態様において前記第2多孔質層に含まれる金属酸化物は、より好ましくは前記金属酸化物Cを含む。前記金属酸化物のスラリー中の濃度は、例えば2質量%以上、15質量%以下であり、好ましくは4質量%以上、13質量%以下である。前記第2多孔質層が複数種の金属酸化物を含む場合には、前記濃度は複数種の金属酸化物の合計濃度を意味する。前記第2多孔質層に含まれる金属酸化物の平均粒径は、例えば0.1μm以上、50μm以下であり、0.3μm以上、30μm以下であり、0.3μm以上、20μm以下であり、0.5μm以上、10μm以下であり、0.5μm以上、5μm以下である。 Examples of the solvent include water and organic solvents. In a preferred embodiment, the metal oxide contained in the second porous layer more preferably contains the metal oxide C. The concentration of the metal oxide in the slurry is, for example, 2 mass% or more and 15 mass% or less, preferably 4 mass% or more and 13 mass% or less. When the second porous layer contains multiple types of metal oxides, the concentration means the total concentration of the multiple types of metal oxides. The average particle size of the metal oxide contained in the second porous layer is, for example, 0.1 μm or more and 50 μm or less, 0.3 μm or more and 30 μm or less, 0.3 μm or more and 20 μm or less, 0.5 μm or more and 10 μm or less, or 0.5 μm or more and 5 μm or less.
前記増粘剤としては、メチルセルロース、ヒドロキシエチルメチルセルロース、ヒドロキシエチルセルロース、ヒドロキシプロピルメチルセルロース、ポリアルキレンオキサイド、ポリビニルアルコール、ポリアクリル酸ナトリウム、ポリビニルピロリドン、ポリアクリルアミド、ポリジメチルアミノエチルメタクリレート等が挙げられる。前記増粘剤のスラリー中の濃度は、例えば0.5質量%以上、5質量%以下であり、好ましくは1質量%以上、3質量%以下である。 Examples of the thickener include methyl cellulose, hydroxyethyl methyl cellulose, hydroxyethyl cellulose, hydroxypropyl methyl cellulose, polyalkylene oxide, polyvinyl alcohol, sodium polyacrylate, polyvinylpyrrolidone, polyacrylamide, polydimethylaminoethyl methacrylate, etc. The concentration of the thickener in the slurry is, for example, 0.5% by mass or more and 5% by mass or less, and preferably 1% by mass or more and 3% by mass or less.
前記撥水剤又は前記撥油剤が塗布された前記第1多孔質層の表面に、前記スラリーを、塗布する方法は特に限定されず、ディップコート法、スプレーコート法、ロールコート法、バーコート法、スピンコート法、スリットコート法、刷毛塗り等が挙げられる。 The method for applying the slurry to the surface of the first porous layer to which the water repellent or oil repellent has been applied is not particularly limited, and examples of the method include dip coating, spray coating, roll coating, bar coating, spin coating, slit coating, brush coating, etc.
前記熱処理の温度は、例えば95℃以上であり、好ましくは265℃以上であり、より好ましくは500℃以上であり、更に好ましくは1000℃以上である。前記熱処理の温度は例えば1600℃以下であり、好ましくは1400℃以下である。前記熱処理の温度が前記金属酸化物Aの軟化温度以上であることが好ましく、具体的には、前記熱処理の温度が1000℃以上、1500℃以下であることが好ましく、1100℃以上、1400℃以下であることがより好ましい。前記熱処理の温度での保持時間は、例えば30分以上、10時間以下であり、好ましくは1時間以上、8時間以下であり、より好ましくは3時間以上、7時間以下である。 The temperature of the heat treatment is, for example, 95°C or higher, preferably 265°C or higher, more preferably 500°C or higher, and even more preferably 1000°C or higher. The temperature of the heat treatment is, for example, 1600°C or lower, preferably 1400°C or lower. The temperature of the heat treatment is preferably equal to or higher than the softening temperature of the metal oxide A, and specifically, the temperature of the heat treatment is preferably 1000°C or higher and 1500°C or lower, and more preferably 1100°C or higher and 1400°C or lower. The holding time at the heat treatment temperature is, for example, 30 minutes or more and 10 hours or less, preferably 1 hour or more and 8 hours or less, and more preferably 3 hours or more and 7 hours or less.
前記多孔質セラミックス積層体は、精密濾過膜として用いることができる。前記多孔質セラミックス積層体における前記第2多孔質層の上に、さらに機能膜を積層することで、前記機能膜が積層された本発明の多孔質セラミックス積層体は、限外濾過膜、ナノ濾過膜、逆浸透膜、イオン交換膜、ガス分離膜等の膜の基材としても用いることができる。 The porous ceramic laminate can be used as a precision filtration membrane. By further laminating a functional membrane on the second porous layer in the porous ceramic laminate, the porous ceramic laminate of the present invention on which the functional membrane is laminated can also be used as a substrate for membranes such as ultrafiltration membranes, nanofiltration membranes, reverse osmosis membranes, ion exchange membranes, and gas separation membranes.
以下、実施例を挙げて本発明をより具体的に説明する。本発明は以下の実施例によって制限を受けるものではなく、前記、後記の趣旨に適合し得る範囲で適当に変更を加えて実施することも勿論可能であり、それらはいずれも本発明の技術的範囲に包含される。 The present invention will be described in more detail below with reference to examples. The present invention is not limited to the following examples, and can of course be modified as appropriate within the scope of the above and below-described aims, and all such modifications are within the technical scope of the present invention.
下記実施例及び比較例で得られたセラミックス積層体は、以下の方法で評価した。 The ceramic laminates obtained in the following examples and comparative examples were evaluated by the following methods.
(1)細孔径の測定
多孔質セラミックス積層体試料を120℃で4時間乾燥した後、オートポアIV9520(micromeritics社製)を用いて、水銀圧入法により測定した。第2多孔質層を積層する前の第1多孔質層、及び、下記実施例の多孔質セラミックス積層体試料を測定すると、横軸を細孔径とするlog微分細孔容積分布において、第2多孔質層を積層する前の第1多孔質層では1つのピークが観測され、下記実施例の多孔質セラミックス積層体では2つのピークが観測された。第2多孔質層を積層する前の第1多孔質層で観測されたピーク位置をDaとした。下記実施例の多孔質セラミックス積層体で観測された2つのピークのうち、低細孔径側のピーク位置をDbとした。
(1) Measurement of pore size After drying the porous ceramic laminate sample at 120 ° C. for 4 hours, the pore size was measured by mercury intrusion using Autopore IV9520 (manufactured by Micromeritics). When the first porous layer before laminating the second porous layer and the porous ceramic laminate sample of the following example were measured, in the log differential pore volume distribution with the pore size on the horizontal axis, one peak was observed in the first porous layer before laminating the second porous layer, and two peaks were observed in the porous ceramic laminate of the following example. The peak position observed in the first porous layer before laminating the second porous layer was taken as D a . Of the two peaks observed in the porous ceramic laminate of the following example, the peak position on the lower pore size side was taken as D b .
(2)第2多孔質層の膜厚の変動係数の測定
円筒形の多孔質セラミックス積層体を樹脂に埋め込み、研磨して、軸方向に垂直な断面(すなわち、第1及び第2多孔質層の積層方向に並行な断面)を出して、走査型電子顕微鏡(SEM、Scanning Electron Microscope)にて観察した。前記第2多孔質層の、前記第1多孔質層側表面の合計長さが円周方向に1.5mm以上となるように画像を取得し、画像解析により第2多孔質層のみを抽出した。得られた画像を8μmピッチで区切って190か所以上の領域とし、それぞれについて面積を求めて8μmで除算した値を各領域における膜厚とした。得られた膜厚から平均値、及び、標準偏差を算出し、標準偏差を平均値で除算することで変動係数を得た。さらに、第2多孔質層の平均膜厚AVE(tb)及び標準偏差σ(tb)を、それぞれ第1多孔質層の細孔径Daで除算した。図1に、実施例2において第2多孔質層の膜厚を測定した際の画像解析の一部を示す。図1中、1は第1多孔質層、2は第2多孔質層、3は測定の間隔(図1では8μm)である。
(2) Measurement of the coefficient of variation of the thickness of the second porous layer A cylindrical porous ceramic laminate was embedded in resin, polished, and a cross section perpendicular to the axial direction (i.e., a cross section parallel to the lamination direction of the first and second porous layers) was taken and observed with a scanning electron microscope (SEM). An image was obtained so that the total length of the first porous layer side surface of the second porous layer was 1.5 mm or more in the circumferential direction, and only the second porous layer was extracted by image analysis. The obtained image was divided at an 8 μm pitch to create 190 or more regions, and the area of each was calculated and divided by 8 μm to obtain the thickness of each region. The average value and standard deviation were calculated from the obtained thickness, and the standard deviation was divided by the average value to obtain the coefficient of variation. Furthermore, the average thickness AVE (t b ) and standard deviation σ (t b ) of the second porous layer were each divided by the pore diameter D a of the first porous layer. Fig. 1 shows a part of the image analysis when the thickness of the second porous layer was measured in Example 2. In Fig. 1, 1 is the first porous layer, 2 is the second porous layer, and 3 is the measurement interval (8 µm in Fig. 1).
(3)空隙率の測定
円筒形の多孔質セラミックス積層体を樹脂に埋め込み、研磨して、軸方向に垂直な断面を出して、走査型電子顕微鏡(SEM、Scanning Electron Microscope)にて観察した。前記第2多孔質層の、前記第1多孔質層側表面の合計長さが円周方向に4.0mm以上となるように画像を取得し画像解析により第2多孔質層のみを抽出した。抽出した第2多孔質層の下側の領域について、前記第2多孔質層の前記第1多孔質層側表面から(すなわち、第2多孔質層の第1多孔質層側の境界から)、第2多孔質に沿って第1多孔質層の細孔径の2倍の領域を画像解析により設定し、解析領域とした。この解析領域内の空隙部分を画像解析で抽出し、空隙部分の面積を解析領域の面積で除算して100倍することで空隙率を得た。図2に、空隙率を測定する方法を模式的に示す。図2中、1は第1多孔質層、2は第2多孔質層、2’は第2多孔質層の第1多孔質層側の境界、4は空隙である。
(3) Measurement of porosity A cylindrical porous ceramic laminate was embedded in resin, polished, and a cross section perpendicular to the axial direction was taken and observed with a scanning electron microscope (SEM, Scanning Electron Microscope). An image was acquired so that the total length of the first porous layer side surface of the second porous layer was 4.0 mm or more in the circumferential direction, and only the second porous layer was extracted by image analysis. For the extracted lower region of the second porous layer, a region twice the pore diameter of the first porous layer was set along the second porous layer from the first porous layer side surface of the second porous layer (i.e., from the boundary of the first porous layer side of the second porous layer) by image analysis, and was set as the analysis region. The void portion in this analysis region was extracted by image analysis, and the area of the void portion was divided by the area of the analysis region and multiplied by 100 to obtain the porosity. FIG. 2 shows a schematic diagram of a method for measuring the porosity. In FIG. 2, 1 is a first porous layer, 2 is a second porous layer, 2' is a boundary of the second porous layer on the side of the first porous layer, and 4 is a gap.
(4)パーミアンスの測定
円筒形の多孔質セラミックス積層体試料の外側から空気を1.0m3/hの一定の流量で流し、前記試料の内側から空気を透過させた。前記試料の透過前後の圧力差を測定した。測定した結果を用いて、下記式によってパーミアンスを算出した。
(4) Measurement of permeance Air was made to flow from the outside of a cylindrical porous ceramic laminate sample at a constant flow rate of 1.0 m3 /h, and the air was allowed to permeate from the inside of the sample. The pressure difference before and after the air permeated the sample was measured. Using the measurement results, the permeance was calculated according to the following formula.
実施例1
第1多孔質層として、アルミナとSiO2を含む萩ガラス社製アルミナ基材A-16を用いた。前記基材A-16の形状は、内径が8.6mm、外径が11.5mm、長さが5cmの円筒形であった。株式会社コロンブス製の撥水剤SHコンク(フッ素樹脂と石油系炭化水素を含む)に前記基材A-16をディップし、常温で12時間以上乾燥させた。次に、住友化学株式会社製のアルミナ粉末AKP-3000と、増粘剤として信越化学工業株式会社製のヒドロキシプロピルメチルセルロース65SH-30000を、それぞれ、5wt%、1.5wt%の濃度で水に混合してスラリーを用意した。なお、前記アルミナ粉末AKP-3000の平均粒径は0.7μmであった。前記基材A-16の内周面に前記スラリーが入り込まないように、前記基材A-16の上端及び下端を封止して、前記スラリーで前記基材A-16をディップコートした。その後、前記外周面に前記スラリーが塗布された前記基材A-16を1200℃で3時間熱処理した。なお、前記撥水剤SHコンクを塗布し乾燥させた後、上記した条件(1)及び(2)の要件を満たしていたことを確認している。
Example 1
As the first porous layer, alumina substrate A-16 manufactured by Hagi Glass Co., Ltd., containing alumina and SiO 2, was used. The shape of the substrate A-16 was a cylinder with an inner diameter of 8.6 mm, an outer diameter of 11.5 mm, and a length of 5 cm. The substrate A-16 was dipped in a water repellent SH Conc (containing fluororesin and petroleum-based hydrocarbons) manufactured by Columbus Co., Ltd., and dried at room temperature for 12 hours or more. Next, alumina powder AKP-3000 manufactured by Sumitomo Chemical Co., Ltd. and hydroxypropyl methylcellulose 65SH-30000 manufactured by Shin-Etsu Chemical Co., Ltd. as a thickener were mixed in water at concentrations of 5 wt% and 1.5 wt%, respectively, to prepare a slurry. The average particle size of the alumina powder AKP-3000 was 0.7 μm. The upper and lower ends of the substrate A-16 were sealed so that the slurry would not get into the inner peripheral surface of the substrate A-16, and the substrate A-16 was dip-coated with the slurry. Thereafter, the substrate A-16 with the slurry applied to the outer peripheral surface was heat-treated at 1200°C for 3 hours. After the water repellent SH Conc was applied and dried, it was confirmed that the requirements of the above conditions (1) and (2) were met.
比較例1
株式会社コロンブス製の撥水剤SHコンクをディップしないこと以外は、前記実施例1と同様にして試料を得た。
Comparative Example 1
A sample was obtained in the same manner as in Example 1, except that the water repellent SH Conc manufactured by Columbus Co., Ltd. was not dipped.
実施例2
第1多孔質層として、アルミナとSiO2を含む萩ガラス社製アルミナ基材A-12を用いた。前記基材A-12の形状は、内径が7.0mm、外径が9.5mm、長さが10cmの円筒形であった。株式会社コロンブス製の撥水剤SHコンクに前記基材A-12をディップし、常温で12時間以上乾燥させた。次に、住友化学株式会社製のアルミナ粉末AKP-3000と、増粘剤として信越化学工業株式会社製のヒドロキシプロピルメチルセルロース65SH-30000を、それぞれ、5wt%、1.5wt%の濃度で水に混合してスラリーを用意した。なお、前記アルミナ粉末AKP-3000の平均粒径は0.7μmであった。前記基材A-12の内周面に前記スラリーが入り込まないように、前記基材A-12の上端及び下端を封止して、前記スラリーで前記基材A-12をディップコートした。その後、前記外周面に前記スラリーが塗布された前記基材A-12を1200℃で3時間熱処理した。前記スラリーの塗布と熱処理をもう一度繰り返して試料を得た。なお、前記撥水剤SHコンクを塗布し乾燥させた後、上記した条件(1)及び(2)の要件を満たしていたことを確認している。
Example 2
As the first porous layer, alumina substrate A-12 manufactured by Hagi Glass Co., Ltd., containing alumina and SiO 2, was used. The shape of the substrate A-12 was a cylinder with an inner diameter of 7.0 mm, an outer diameter of 9.5 mm, and a length of 10 cm. The substrate A-12 was dipped in a water repellent SH Conc manufactured by Columbus Co., Ltd., and dried at room temperature for 12 hours or more. Next, alumina powder AKP-3000 manufactured by Sumitomo Chemical Co., Ltd. and hydroxypropyl methylcellulose 65SH-30000 manufactured by Shin-Etsu Chemical Co., Ltd. as a thickener were mixed in water at concentrations of 5 wt% and 1.5 wt%, respectively, to prepare a slurry. The average particle size of the alumina powder AKP-3000 was 0.7 μm. The upper and lower ends of the substrate A-12 were sealed so that the slurry would not enter the inner peripheral surface of the substrate A-12, and the substrate A-12 was dip-coated with the slurry. Thereafter, the substrate A-12 with the slurry applied to the outer peripheral surface was heat-treated at 1200° C. for 3 hours. The application of the slurry and the heat treatment were repeated once more to obtain a sample. It was confirmed that the above-mentioned conditions (1) and (2) were satisfied after the water repellent SH Conc was applied and dried.
比較例2
株式会社コロンブス製の撥水剤SHコンクをディップしないこと以外は、前記実施例2と同様にして試料を得た。
Comparative Example 2
A sample was obtained in the same manner as in Example 2, except that the water repellent SH Conc manufactured by Columbus Co., Ltd. was not dipped.
実施例及び比較例について、上記した(1)~(4)に従って測定した結果を表1に示す。 The results of measurements taken in accordance with (1) to (4) above for the Examples and Comparative Examples are shown in Table 1.
表1において、実施例1と比較例1を対比すると、第2多孔質層の膜厚の変動係数が0.35以下である実施例1では良好なパーミアンスを実現していたのに対し、前記変動係数が0.35を超えていた比較例1では、実施例1に比べてパーミアンスが劣る結果となった。また、撥水剤を用いないこと以外は実施例2と同様にして積層体を作成した比較例2では、第2多孔質層が形成できなかったのに対し、実施例2では膜厚の変動係数が0.35以下である第2多孔質層を形成することができ、良好なパーミアンスを実現できた。 Comparing Example 1 and Comparative Example 1 in Table 1, Example 1, in which the coefficient of variation of the film thickness of the second porous layer was 0.35 or less, achieved good permeance, whereas Comparative Example 1, in which the coefficient of variation exceeded 0.35, achieved poorer permeance than Example 1. In Comparative Example 2, in which a laminate was prepared in the same manner as Example 2 except that no water repellent agent was used, the second porous layer could not be formed, whereas Example 2 was able to form a second porous layer with a coefficient of variation of the film thickness of 0.35 or less, achieving good permeance.
Claims (3)
前記第2多孔質層は、前記第1多孔質層の上に接して積層されている部分と、前記第1多孔質層の上に空気を介して積層されている部分を有し、
前記第2多孔質層の膜厚の変動係数CV(tb)が0.05以上0.35以下であり、
前記第2多孔質層の膜厚の標準偏差σ(t b )を、前記第1多孔質層の平均細孔径D a で除した値(σ(t b )/D a )が0.2以上0.8以下であり、
前記第2多孔質層の膜厚の平均値AVE(t b )を、前記第1多孔質層の平均細孔径D a で除した値(AVE(t b )/D a )が0.5以上5以下であり、
前記第1多孔質層と前記第2多孔質層の界面における空隙率が29.0%以上55%以下であり、
前記第2多孔質層の平均細孔径D b に対する前記第1多孔質層の平均細孔径D a の比(D a /D b )が10以上200以下であり、
前記変動係数CV(t b )及び膜厚の標準偏差σ(t b )は、下記の要領で求められる値であることを特徴とする多孔質セラミックス積層体。
(i)前記第1多孔質層と第2多孔質層の積層方向に平行な断面の画像を取得する。
(ii)前記画像において、前記第2多孔質層の、第1多孔質層側表面の合計長さが、前記第1多孔質層の平均細孔径の100倍以上となるように画像を取得する。
(iii)画像解析により第2多孔質層のみを抽出し、得られた画像を一定間隔で区切って190か所以上の領域とし、各領域の面積を求めて、区切った間隔の長さで除した値を各領域における第2多孔質層の膜厚とする。ただし、区切った間隔の長さは第1多孔質層の平均細孔径の1.8倍以下の長さとする。
(iv)測定した全領域についての膜厚の平均値AVE(t b )、膜厚の標準偏差σ(t b )を求める。
(v)前記膜厚の標準偏差σ(t b )を前記膜厚の平均値AVE(t b )で除すことにより前記膜厚の変動係数CV(t b )を求める。 A porous ceramic laminate having a first porous layer and a second porous layer laminated on the first porous layer,
the second porous layer has a portion laminated on and in contact with the first porous layer and a portion laminated on the first porous layer with air interposed therebetween;
the coefficient of variation CV(t b ) of the thickness of the second porous layer is 0.05 or more and 0.35 or less ;
a value (σ(t b )/D a ) obtained by dividing a standard deviation σ(t b ) of a thickness of the second porous layer by an average pore diameter D a of the first porous layer is 0.2 or more and 0.8 or less;
a value (AVE(t b )/D a ) obtained by dividing an average thickness AVE(t b ) of the second porous layer by an average pore diameter D a of the first porous layer is 0.5 or more and 5 or less,
a porosity at an interface between the first porous layer and the second porous layer is 29.0% or more and 55% or less;
a ratio (D a /D b ) of an average pore diameter D a of the first porous layer to an average pore diameter D b of the second porous layer is 10 or more and 200 or less;
A porous ceramic laminate, wherein the coefficient of variation CV(t b ) and the standard deviation σ(t b ) of the film thickness are values that can be determined as follows :
(i) An image of a cross section parallel to the lamination direction of the first porous layer and the second porous layer is obtained.
(ii) The image is acquired so that the total length of the surface of the second porous layer facing the first porous layer is 100 times or more the average pore diameter of the first porous layer.
(iii) Extract only the second porous layer by image analysis, divide the obtained image at regular intervals into 190 or more regions, calculate the area of each region, and divide the area by the length of each divided region to obtain the film thickness of the second porous layer in each region, where the length of each divided region is 1.8 times or less the average pore diameter of the first porous layer.
(iv) The average film thickness AVE(t b ) and the standard deviation σ(t b ) of the film thickness for the entire measured region are calculated .
(v) The standard deviation σ(t b ) of the film thickness is divided by the average film thickness AVE(t b ) to obtain the coefficient of variation CV(t b ) of the film thickness .
前記第1多孔質層の少なくとも一方の表面に、撥水撥油剤を塗布する工程を含み、
前記撥水撥油剤は、下記の条件(1)及び(2)が満たされるように塗布される多孔質セラミックス積層体の製造方法。
(1)撥水撥油剤を前記第1多孔質層の少なくとも一方の表面に塗布し、乾燥後、前記第1多孔質層の撥水撥油剤塗布面(両面に塗布される場合にはいずれか一方の塗布面)から空気を1.0m3/hの流量で流した際、空気を流した面と反対側の面から少なくとも0.8m3/h以上の流量の空気が流れる。
(2)撥水撥油剤を前記第1多孔質層の少なくとも一方の表面に塗布し、乾燥後、前記第1多孔質層の撥水撥油剤塗布面(両面に塗布される場合にはいずれか一方の塗布面)から空気を1.0m3/hの流量で流した際、空気を流す試験前後の重量減少率が0.1%以内である。 A method for producing the porous ceramic laminate according to claim 1 or 2 , comprising the steps of:
applying a water- and oil-repellent agent to at least one surface of the first porous layer;
The water- and oil-repellent agent is applied so as to satisfy the following conditions (1) and (2):
(1) A water- and oil -repellent agent is applied to at least one surface of the first porous layer, and after drying, when air is caused to flow at a flow rate of 1.0 m3 /h from the water- and oil-repellent agent-coated surface of the first porous layer (or from either surface if coated on both surfaces), air flows at a flow rate of at least 0.8 m3 /h from the surface opposite to the surface through which the air is flowing.
(2) A water- and oil -repellent agent is applied to at least one surface of the first porous layer, and after drying, air is passed through the water- and oil-repellent coated surface of the first porous layer (or through either one of the coated surfaces if coated on both surfaces) at a flow rate of 1.0 m3 /h; the weight loss rate before and after the air passage test is within 0.1%.
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| CN202180028954.1A CN115427375A (en) | 2020-04-22 | 2021-03-30 | Porous ceramic laminate and method for producing same |
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